Lubricant compositions



United States Patent US. Cl. 252-45 5 Claims ABSTRACT OF THE DISCLOSURE Low molecular weight 1,3 polymers of 3 methylbutene-l are suitable as lubricant base stocks.

This is a division of application Ser. No. 366,189, filed May 8, 1964.

This invention relates to lubricants containing the 1,3 polymer of 3-methylbutene-l.

For many years, lubricating oils have been prepared from petroleium distillate fractions by various refining techniques. To meet qualifications required by certain applicatons, additives have been incorporated to improve oxidation stability, viscosity index, pour point, and many other properties.

In recent years, the more stringent requirements imposed on lubricating oils have prompted research related to entirely new kinds of oils. New, more stable molecules which can provide satisfactory lubrication over wide temperature ranges, for example 65 F. to as high as 500 F are required. Automobile manufacturers are consistently recommending longer intervals between services for new cars. Since conventional mineral oils are not always satisfactory for these applications, various synthetic oils have been investigated.

Possibly one of the earliest areas of investigation of synthetic lubricants or synthesized hydrocarbon additives is that of polyolefins. Polyisobutylene, for example, has been used as a synthetic oil for over 30 years. Even after hydrogenation, polyolefins generally were unsatisfactory lubricants because of one or more limiting deficiencies, often attributable to the structure of the polymer itself. For example, polyisobutylene, before or after hydrogenation, has relatively poor viscosity-temperature characteristics and is susceptible to degradation by heat. These undesirable characteristics are believed to be caused, at least in part, by the rigid, strained nature of the polyisobutylene molecule, a result of the repulsion or crowding of the gem-dimethyl groups on alternate carbon atoms in the main chain.

W I W iii/ h Polyisobutylene Polypropylene Polyethylene Polypropylene, while not having the rigid nature of the polyisobutylene molecule, has tertiary hydrogen atoms at each second carbon of the main chain (see skeletal diagram). These tertiary hydrogens are potential sites for severe oxidative attack. Ethylene polymers have very high pour points attributable to the lack of side chains. Polymers of higher alpha-olefins are deficient for various reasons; in general, they have quite low viscosities or break down very rapidly in shear gradients.

It has now been discovered that the 1,3 polymer of 3-methylbutene1 is an excellent lubricating oil constituent. This polymer, which can be realized only under 3,484,857 Patented Dec. 16, 1969 certain special conditions of polymerization, provides lubricating oil constituents which possess excellent thermal, shear, and oxidation stability. The polymer may be used as a base stock, a viscosity index improver, or a building block for a larger molecule, such as a detergent.

The 1,3 polymer of 3-methylbutene-1 is obtained by polymerizing in such a manner that the 1, 2 and 3 car bon atoms all become part of the chain, rather than only the 1 and 2 carbon atoms as is the case in the 1,2 polymer. In order to obtain this 1,3 polymer, a hydride shift must occur from carbon atom 3 to carbon atom 2 for each monomer adding to the main chain. A hydride ion is a hydrogen atom with two electrons. The hydride shift mechanism is as follows:

N A 6 Y 1.3 polymer of 3metl1ylbutene-1 Hydride shift polymers of 3-methylbutene-1 have been reported by Kennedy and Thomas, Makromolekulare Chemie, vol 53, p. 28 (1962) and vol. 64, p. 1 (1963). These polymers were crystalline materials of high molecular weights (about 50,000) obtained over very active Friedel-Crafts catalysts (e.g., AlCl at temperatures of C. and below. The crystallinity and high molecular Weights of these polymers, of course, preclude their use as lubricants and limit their use in oil additives. Al though in theory polymers of lower molecular weight could be made by operating at higher temperatures, strongly acidic catalysts such as AlCl become isomerization catalysts at temperatures of 0 C. and above; furthermore, it is indicated in the articles by Kennedy and Thomas that 1,2 polymerization rather than 1,3 polymerization was obtained at higher temperatures.

The superior properties of the 1,3 or hydride-shift polymer of 3-methylbutene-1 as compared with polyisobutylene probably derive from the insertion of another methylene group between the quaternary carbon atoms. This extra methylene group provides further separation of the gem-dimethyl groups, thus relieving molecular crowding or strain and providing a more flexible molecule. Therefore, the instant polymer has excellent shear resistance as well as a lower pour point, good oxidation stability, etc. Accordingly, it is essential that a high pro portion but not all of the polymer have a 1,3 structure rather than the 1,2 structure obtained in conventional polymerizations. The 1,2 polymer can be described as an ethylene chain with isopropyl groups attached to every other carbon atom in the chain. The skeletal diagram of the 1,2 polymer of 3-methylbutene-1 is compared with that of the 1,3 polymer below 1,3 polymer 1,2 polymer It is apparent that the 1,2 polymer is very oxidationunstable because of the presence of tertiary hydrogens on both the main chain and the side group. Therefore, a preponderance (i.e., at least 50%) of 1,3 linkages is essential to the polymers of the invention. The repeating unit of the 1,3 polymer is It is preferred that from about 60 to 98%, and more desirably 80 to 95% of the polymerizing molecules of 3-methylbutene-1 have their 1, 2, and 3 carbon atoms become part of the chain; i.e., from 60 to 98% and preferably 80 to 95% of the polymerization is hydride-shift polymerization. The remainder is made up of 1,2 linkages, and groups derived from the catalyst or solvent, cyclized units, and unsaturated end groups formed by hydride removal.

There are three general areas of applicability of the present polymers in lubricating oils. They may be used (1) as oil base stocks (after hydrogenation), (2) as viscosity-index improvers (generally also after hydrogenation), and (3) as building blocks for larger molecules which require a stable, long hydrocarbon chain, such as dispersants. When used as base stocks, the hydride-shift polymers are generally preferred to be in the molecular weight range of from about 200 to about 4000, preferably 300 to 2000. These base oils generally comprise at least 50% by weight and usually 80% or more of the oil composition; however, these polymers are soluble in mineral oils and can be mixed therewith in any concentration. It is preferred to use at least 30% by weight of the 1,3 polymer of 3-methylbutene-1, more preferably at least 60%. When used as a base stock, any of the well known additives may be added to provide improved viscosity index, pour point, oxidation stability, etc.

When used as viscosity-index improvers in mineral oils, hydride-shift polymers of 3-methylbutene-1 are generally preferred to be in the molecular weight range of from about 10,000 to 500,000, preferably 10,000 to 200,000. These long-chain polymers can be used to increase the VI of any mineral oil or other polymer-based oil. Although the theory of VI improvement is not completely understood, it is believed to relate to a change in the physical state of solution or dispersion of the polymer molecules with a change in temperature. Desirable concentrations of the instant polymer when used as a VI improver are from about 1 to about preferably 2 to 8% by weight of the lubricating oil.

As an example of the use of the instant polymer as a VI improver, a solution of 1.5% wt. of poly-3-methylbutene-l, 10,000 molecular weight, and about 80% 1,3 linkages in a mixture of neutral mineral oils had the following viscosities:

Viscosity of base Dispersant additives, commonly known as detergents, are widely used in concentrations of from about 0.2 to 10% by weight to impart properties to oils which enable oxidation products, soots, resins, and other insoluble mat ter to remain in suspension or dispersion so that they will not adhere to metal surfaces to build up as sludge or vanish deposits. Dispersants may be made from the instant polymer by attaching polar groups, preferably nitrogen-containing polar groups, at the unsaturated end. Preferred polar groups contain only carbon, hydrogen, nitrogen, and a chaloogen, preferably oxygen. Molecular weights of the polar group are from about 100 to about 3000. Although it is preferred to have only one polymer chain attached to each polar group, it is also possible to have two or more chains attached to the group. Preferred polar groups contain at least 1, preferably 1 to 3 heterocyclic groups having from 5 to members in each heterocyclic group; for example derivatives of pyridine, pyrazine, pyrrolidone, pyrrolidine,, succinimide, oxazine, quinoline, morpholine, thiophene, etc. Members of the heterocyclic group are preferably selected from the group consisting of carbon, nitrogen, oxygen, and sulfur. Examples of suitable polar groups are the maleic anhydride-polyethylene imine adducts where x=1 to 10. Molecular weights of the poly(3-methylbutene-l) suitable for this purpose are generally preferred to be in the range 200 to 10,000, preferably 500 to 3000. The adduct is formed by first reacting the poly 3-methylbutene-1 with maleic anhydride, then with a polyethylene imine of the desired molecular weight, preferably tetraethylene pentamine. Molecular weights of the dispersant generally range from about 200 to about 12,000, preferably 400 to 8000. Variants on the structure above include 1) adduct in which the C 0 double bond is hydrogenated, (2) adduct in which an alkenyl succinimide unit occurs at both ends of the polyimine chain, (3) adduct in which the imide structure is cyclized t0 imidazoline, (4) adduct in which the carbonyl groups are reduced to CH (5) adduct which is formed by reacting poly-3-methylbutene-l with HCl or HBr to obtain a long-chain alkyl halide, then using that alkyl halide to alkylate polyethylene imine, (6) adduct formed by reacting the formamide o HQCH2CHZ(NHCHZCH2) II with the terminally unsaturated poly-3-methylbutene-1 in the presence of ultraviolet light.

To illustrate the superior properties of the polymer of the invention, oxidation and thermal stability comparisons were made with polyisobutylene.

EXAMPLE I Weight loss 2.5% 5.0% 10% 15% 20% Polyisobutylcne, O 280 292 308 319 32 3niethylbutene-1, C 315 345 401 407 41 The data indicate that higher temperatures are necessary to decompose given amounts of poly(3-methylbutene-1) than polyisobutylene; thus, the 1,3 polymer of 3-methylbutene-l is a more thermally stable material. Indeed, these results are conservative in that the lower mole weight polymer would be expected to show somewhat higher weight losses than the higher mole weight material.

EXAMPLE II Tetrahaloaluminate catalysts can be employed 'in any fashion known to those skilled in the art; for example, the catalyst can be powdered and used as a solid (at temperatures below the melting point of the salt), or can be used as a molten salt catalyst or supported on an inert carrier, such as porcelain, alumina, or charcoal. Monomer can be fed with or without a solvent to a reactor which contains the catalyst. If the catalyst is in the solid i' f g ggg ig iii g i g ggfi g gi gg form, the catalyst may be retained in the reactor or pait 10,000. The molcular weights oi the polyethylene and gg g g igg g l i;$ 12362:52 22; f if g g zi gb f ,gggs were about 20000 and respec rated and recycled or discarded, or may be allowed to Polymer oxidation was measured by the liters of oxygen pass out Wlth the product If the catalyst used m the molten form, it may be separated from the reactor g i? per 500 9 f 100 hours of 15 effluent (in which it is substantially insoluble) and reub mg oxygen t roub e Samp cycled or discarded. Generally, any substance in which Liters O (NTP)/500 the reactants are soluble and which does not take part in Oxidation stabilities of a linear polyethylene, a polyisobutylene and poly(3-methylbutene-l) were determined by oxygen absorption tests conducted at 165 C. on 10% w. solutions of polymer in a solvent of bis(p-phenoxyphenyl) ether having about two ter t-butyl substituents per molecule containing 0.20% W. copper naphthenate catagrams solution absorbed the reaction is a suitable solvent; as examples, mention Polymer: in 100 hours may be made of parafiins, such as isooctane; halogenated Poly(3-rnethylbutene-l) alkanes, such as methyl and ethyl chlorides, and methyl Polyethylene 9 and ethyl bromides; 1,2-dichloroethane, carbon disulfide, Polyisobutylene nitrobenzene, nitromethane, vinyl chloride, etc. It is pre- The lower oxygen uptake by the pbly(3 methylbutene l) ferred to carry out the reaction in the presence of a solindicates the superior oxidation resistance of this polymer. t bacauge dllutlon of the i Shows i The 3-methylbutene-l polymer 5f the invention can be ,rate h mI 10mer relatlve to the hydn de shlft prepared in several ways; however, it is essential that reacnon msurmg: a h Percentage of llydndeshlft P 3" polymerization takes place in such a manner that the Furfharmoler 1t 15 generally to handle l product predominates in 1,3 polymen Very high mo1ec polymer in solution. When a solvent is used, volumetric u1ar weight (eigw Solid and Semi s1id) 3 1 can solvent/monomer ratios are from about 0.5 to about 20, be produced at low temperatures with Friedel-Crafts cat- Preferably F 1 about 1 to a ut 10. alysts. These high-molecular-weight materials can then P lym rization temperatures with M(AlX catalysts be cracked by well known methods to yield polymers ar usually in the range of from about 50 C. to about suitable for use in lubricating oils. For example, the poly- 120 C. preferably from about 0 to about 100 C., de-

mer of molecular weight 50,000 may be heated under pending on the concentration of the monomer and the high Vacuum at 5 C- for fifteen minutes to give polydesired molecular weight of the polymer. The polymerizamer of about 1000 molecular weight. Preparation of the tion is carried out in the liquid phase. Process pressures high-m mammals 1S descflbed 1n detall 1B are not critical, except to keep the system substantially in the Kennedy and homas artICleS noted abovethe liquid phase; autogenous pressures are generally satis- Predominantly hydride-shift polymers of 3-methylfactory butene-l can also be prepared by polymerization over Pol mers re ared with M AlX cat 1 tetrahaloaluminate catalysts havmg the formula y P p on a ysts are pre ferred for use in lubricating oils because these catalysts M(A1X produce the desired polymer directly; cracking of highwherein M is a metal or a mixture of metals, especially molecuiar'welgllt Polymsrs is Sometimes CCoInpanied by a metal from group I H VIII of the Periodic Table other side reactions, such as rearrangement, which proespecially Li, Na, and Co; 11 is a whole number equal to 11106 undeslrefl Propemes the Product the valence of M (i.e., n is one if M is monovalent, two The following table illustrates the results of 3-methylif M i divalent, gtg) and X i a halogen, f bl butene-1 polymerization over various tetrahaloaluminate chlorine, bromine or iodine. Tetrahaloaluminates are catalysts. Product structure was determined by nuclear white to greyish, brittle, low-melting crystalline solids. gnet c reson nce and confirmed by infrared analyses Some examples of these compounds are NaAlCl to be at least about 80% 1,3 polymer in each case.

POLYMERIZATION OF 3-MEIHYLBUTENE-l WITH HYDRIDE SHIFT OVER TETRAHALOALUMINATE SALTS Experiment Number 3-methylbutene-1 (I) mmoles 799 442 539 372 538. Solvent (II) A. One Il-CsHii--. n' BH14--- Isooetane-.-. 1,2-C2H4Clz... 1,2-C2H4Cl2 Isooctane. Solvent, mmoles 30 47 Catalyst (111)"-.. Catalyst, mmoles 4 Order of addition Temperature, 0.3;5 Pressure, p.s.i.g.:l:5

Time, hr Recovery of charge, percent 99.6 103. Yield of finished polymer. w. of feed, no es ba ea. 1 5 17. 6 17. 5 27. 2. Polymer Molecular Weight (ebullioscopic l, 1003: (600-800) (400*500) (800-1, 000) Experiments 1-3 were made in a stirred glass reactor with internal cooling coil; experiments 4'7 were made in a 250 ml. stainless steel autoclave.

In the latter series, 3-methylbutene-1 was fed slowly and continuously by means of a high pressure syringe pump.

b Described in Daniels et al., Expcrimiental Physical Chemistry, 1949, pp. -79. 0 Catalyst added as suspension in all or part of total solvent, 5 mg. catalyst/ml. of solvent. d Monomer added uniformly during entire run period. 8 Estimated visually by comparison with samples of known molecular weight.

LiAlCI Co(AlCl AgAlCl NaAlBr Be(AlBr Lubricating compositions of the invention may also Mg(AlCl Fe(AlCl Ni(AlBr LiAlI etc. Hycontain any well known additives such as oxidation inhibidride-shift polymerization of 3-methylbutene-1 with these tors, VI improvers, extreme pressure agents, pour point catalysts is described in copending application Ser. No. depressants, antiwear agents, foam inhibitors, corrosion 314,910, filed Oct. 9, 1963, now abandoned. 75 inhibitors, etc.

I claim as my invention:

1. A lubricant composition containing a major amount of hydrogenated poly(3-methylbutene-1) having a molecular weight of from about 300 to about 2000 in which a major proportion of the polymer consists of CH I 3 CH2GOHzunits 2. The composition of claim 1 in which 60 to 98% of the polymer consists of 3. The composition of claim 1 in which 80 to 95% of the polymer consists of 4. A lubricant composition comprising a major amount of a mineral lubricating oil and from about 0.2 to by weight of a dispersant consisting essentially of the addition product of a poly(3-methylbutene-1) in which a major proportion of the polymer consists of units and a nitrogen-containing polar group, said polar group having a molecular weight from about 100 to 3000 and being selected from the group consisting of pyridine, pyrand a nitrogen-containing polar group, said polar group having a molecular Weight from about to 3000 and being a succinamide group, and said dispersant having a molecular weight of from about 200 to about 12,000.

References Cited UNITED STATES PATENTS 2,830,106 4/1958 Good et a1 25259 X 3,154,560 10/1964 Osuch 25251.5 X 3,251,819 5/1966 Kefley 26093.7 3,261,821 7/1966 Vandenberg 26093.7 3,299,022 1/1967 Edwards 260-937 3,349,148 10/ 1967 Bush 252-59 X DANIEL E. WYMAN, Primary Examiner W. CANNON, Assistant Examiner U.S. Cl. X.R. 

